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 Dortmund Data Bank
Thermophysical Data for Process Design
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Query
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DDB# Name CAS-RN Formula
174 Water 7732-18-5 H2O Overview Details
546 Monoethanolamine 141-43-5 C2H7NO Overview Details
1050 Carbon dioxide 124-38-9 CO2 Overview Details
1056 Nitrogen 7727-37-9 N2 Overview Details
2187 Methyldiethanolamine (MDEA) 105-59-9 C5H13NO2 Overview Details
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Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 54 518 273-473 K2-29420 kPa
174 546 1050
7
174 546 2187
3
174 1050 1056
22
174 1050 2187
22
Gas Solubilities GLE 683 5309 273-473 K0-19954 kPa
174 546 1050
291
174 546 1050 2187
69
174 1050 2187
323
Heat Capacities of Mixtures, Excess Heat Capacities CPE 24 266 298-353 Kn.a.
174 546 1050
5
174 546 1050 2187
3
174 546 2187
12
174 1050 2187
4
Solid-Liquid Equilibria SLE 1 32 253-272 Kn.a.
174 546 2187
1
Densities and Volumes of Mixtures, Excess Volumes VE 63 486 293-423 K101-808 kPa
174 546 1050
5
174 546 2187
42
174 1050 2187
16
Mixture Viscosities VIS 182 1884 293-423 K100-400 kPa
174 546 1050
118
174 546 1050 1056
1
174 546 1050 2187
15
174 546 2187
23
174 1050 2187
25
Mixture Surface Tensions MSFT 95 783 293-448 K100-40000 kPa
174 546 1050
34
174 546 1050 2187
23
174 546 2187
13
174 1050 1056
17
174 1050 2187
8
Mixture P-v-T Data MPVT 19 494 293-423 K5-13810 kPa
174 546 1050 1056
1
174 1050 2187
18
Gas Hydrate Data GHD 64 462 272-289 K100-55110 kPa
174 1050 1056
64
Electrical Conductivities ECND 4 20 298 K (const.)100 kPa (const.)
174 546 1050
4
Diffusion Coefficients DIF 11 89 288-337 Kn.a.
174 546 1050
5
174 1050 2187
6
Further Thermodynamic Properties X 349 20478 278-423 K1-20000 kPa
174 546 1050
121
174 546 1050 1056
12
174 546 1050 1056 2187
1
174 546 1050 2187
15
174 546 1056
1
174 1050 1056
3
174 1050 1056 2187
9
174 1050 2187
187
Total 1549 30821
174 546 1050
590
174 546 1050 1056
14
174 546 1050 1056 2187
1
174 546 1050 2187
125
174 546 1056
1
174 546 2187
94
174 1050 1056
106
174 1050 1056 2187
9
174 1050 2187
609

Dortmund Data Bank Version: February 2024
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